TY - JOUR
T1 - Size and exergy assessment of solid oxide fuel cell-based H2-fed power generation system with alternative electrolytes
T2 - A comparative study
AU - Sadeghi, Mohsen
AU - Jafari, Moharram
AU - Hajimolana, Yashar S.
AU - Woudstra, Theo
AU - Aravind, P. V.
PY - 2021
Y1 - 2021
N2 - This work aims to analyse and compare the thermodynamic performance and size of two types of solid oxide fuel cell (SOFC)-based plants. The former is the conventional H2-fed plant based on SOFC with an oxygen-ion conducting electrolyte (SOFC-O), and the latter is based on SOFC using a proton-conducting electrolyte (SOFC-H). Thermodynamic analysis reveals that in the SOFC-H system, due to H2O formation at the cathode side, not only the anode concentration losses decreases, but also the partial pressure difference between H2 and H2O increases which leads to an increase in Nernst voltage compared to the SOFC-O system. Due to this, SOFC-H and SOFC-O based plants exhibit different performance in terms of the cell voltage, power, efficiency, stack outlet temperature and size of heat exchangers used for preheating the fuel and air. The results indicate, for current densities less than around 3,000 A/m2, the energy and exergy efficiencies of SOFC-H-based system are more than those of the SOFC-O-based plant. This results in reduced area of heat exchangers per unit power used in the SOFC-H-based plant as compared with the SOFC-O-based plant. In addition, the sensitivity analysis demonstrates that using thin cells in the SOFC stack is favourable for the SOFC-H-based plant.
AB - This work aims to analyse and compare the thermodynamic performance and size of two types of solid oxide fuel cell (SOFC)-based plants. The former is the conventional H2-fed plant based on SOFC with an oxygen-ion conducting electrolyte (SOFC-O), and the latter is based on SOFC using a proton-conducting electrolyte (SOFC-H). Thermodynamic analysis reveals that in the SOFC-H system, due to H2O formation at the cathode side, not only the anode concentration losses decreases, but also the partial pressure difference between H2 and H2O increases which leads to an increase in Nernst voltage compared to the SOFC-O system. Due to this, SOFC-H and SOFC-O based plants exhibit different performance in terms of the cell voltage, power, efficiency, stack outlet temperature and size of heat exchangers used for preheating the fuel and air. The results indicate, for current densities less than around 3,000 A/m2, the energy and exergy efficiencies of SOFC-H-based system are more than those of the SOFC-O-based plant. This results in reduced area of heat exchangers per unit power used in the SOFC-H-based plant as compared with the SOFC-O-based plant. In addition, the sensitivity analysis demonstrates that using thin cells in the SOFC stack is favourable for the SOFC-H-based plant.
KW - Exergy
KW - Heat exchanger size
KW - Oxygen ion-conducting electrolyte
KW - Proton-conducting electrolyte
KW - Solid oxide fuel cell (SOFC)
UR - http://www.scopus.com/inward/record.url?scp=85097375706&partnerID=8YFLogxK
U2 - 10.1016/j.enconman.2020.113681
DO - 10.1016/j.enconman.2020.113681
M3 - Article
AN - SCOPUS:85097375706
SN - 0196-8904
VL - 228
JO - Energy Conversion and Management
JF - Energy Conversion and Management
M1 - 113681
ER -